CN102603032A - Waste oil separation device - Google Patents
Waste oil separation device Download PDFInfo
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- CN102603032A CN102603032A CN2012100957199A CN201210095719A CN102603032A CN 102603032 A CN102603032 A CN 102603032A CN 2012100957199 A CN2012100957199 A CN 2012100957199A CN 201210095719 A CN201210095719 A CN 201210095719A CN 102603032 A CN102603032 A CN 102603032A
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- 238000000926 separation method Methods 0.000 title abstract description 17
- 239000002699 waste material Substances 0.000 title description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 46
- 239000010865 sewage Substances 0.000 claims abstract description 22
- 239000010802 sludge Substances 0.000 claims description 3
- 238000002485 combustion reaction Methods 0.000 claims 3
- 238000007599 discharging Methods 0.000 claims 1
- 239000013049 sediment Substances 0.000 abstract description 10
- 238000007667 floating Methods 0.000 abstract description 7
- 230000000694 effects Effects 0.000 abstract description 5
- 239000007788 liquid Substances 0.000 abstract description 3
- 239000003921 oil Substances 0.000 description 58
- 235000019198 oils Nutrition 0.000 description 54
- 239000002245 particle Substances 0.000 description 7
- 238000005238 degreasing Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 230000001105 regulatory effect Effects 0.000 description 4
- 239000002351 wastewater Substances 0.000 description 3
- 238000004581 coalescence Methods 0.000 description 2
- 239000013527 degreasing agent Substances 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000003208 petroleum Substances 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 239000011269 tar Substances 0.000 description 2
- 238000009736 wetting Methods 0.000 description 2
- 239000004743 Polypropylene Substances 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- 239000010775 animal oil Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003225 biodiesel Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000003670 easy-to-clean Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000005188 flotation Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000008206 lipophilic material Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000003209 petroleum derivative Substances 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- -1 polypropylene Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 235000015112 vegetable and seed oil Nutrition 0.000 description 1
- 239000008158 vegetable oil Substances 0.000 description 1
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Abstract
Description
技术领域 technical field
本发明涉及一种油水分离设备,尤其涉及一种地沟油回收利用的分离装置。 The present invention relates to an oil-water separation device, in particular to a separation device for recycling waste oil.
背景技术 Background technique
传统地沟油的收集是通过多级油池的长时间的沉降选浮后人工采集,存在效率低、工作繁琐和环境恶劣的问题。 The traditional collection of waste oil is manual collection after long-term sedimentation and flotation in multi-stage oil pools, which has the problems of low efficiency, cumbersome work and harsh environment.
发明内容 Contents of the invention
为了克服现有技术的上述缺点,本发明提供一种采用浅池沉淀理论、旋流分离原理和润湿聚结原理以及斜板除油,提高了单位池容的分离表面,使油水分离的效果得到提高的地沟油分离装置。 In order to overcome the above-mentioned shortcomings of the prior art, the present invention provides a method that adopts the theory of shallow pool sedimentation, the principle of cyclone separation, the principle of wetting and coalescence, and the principle of inclined plate oil removal, which improves the separation surface of the unit pool volume and separates oil from water. Improved gutter oil separation device.
本发明解决其技术问题所采用的技术方法是:一种地沟油分离装置,有调节池、除油罐和连接管路,所述调节池底部设有漏斗状沉渣斗,在漏斗状沉渣斗的底部安装有排污阀;在调节池底下部安装有压力控制阀和油污水管,在油污水管的内端通过软管连接有浮体入口,所述油污水管外端安装有阀门和管路,该管路与上述除油罐底部的油污水入口相接;所述污水入口通过管路与安装在除油罐的内腔中内罐上的旋流器相通,在内罐外周与除油罐内腔壁之间安装有斜板除油器,所述内罐底部设有压回水入口,所述内罐上部设有排水口,该排水口连接管路穿过除油罐罐体与外面相通,所述除油罐的上部设有溢流槽,在溢流槽底部设有排油口,所述除油罐的底部设有排污泥口。 The technical method adopted by the present invention to solve its technical problem is: a kind of sewer oil separation device has a regulating tank, a degreasing tank and a connecting pipeline, the bottom of the regulating pond is provided with a funnel-shaped sediment bucket, and the bottom of the funnel-shaped sediment bucket is A sewage valve is installed at the bottom; a pressure control valve and an oily sewage pipe are installed at the bottom of the regulating tank, and the inner end of the oily sewage pipe is connected to the inlet of the floating body through a hose, and a valve and a pipeline are installed at the outer end of the oily sewage pipe. It is connected with the oily sewage inlet at the bottom of the oil removal tank; the sewage inlet is communicated with the cyclone installed on the inner tank in the inner cavity of the oil removal tank through a pipeline, and the outer periphery of the inner tank is connected with the inner cavity wall of the oil removal tank. A sloping plate degreaser is installed between them, the bottom of the inner tank is provided with a pressure return water inlet, and the upper part of the inner tank is provided with a drain port, and the drain port is connected to the outside through the tank body of the degreasing tank. The upper part of the oil removal tank is provided with an overflow tank, and the bottom of the overflow tank is provided with an oil discharge port, and the bottom of the oil removal tank is provided with a sludge discharge port.
所述漏斗状沉渣斗斜面夹角为45度。 The included angle of the slope of the funnel-shaped sediment bucket is 45 degrees.
本发明的有益效果是:利用污水流经装置时形成的液位差,实现油水分离,能缩短废水停留时间,减小了设备容积,油水分离效果好,占地面积小,纯机械设计,结构简单,稳定性好。 The beneficial effects of the present invention are: the liquid level difference formed when the sewage flows through the device is used to realize the oil-water separation, the residence time of the waste water can be shortened, the volume of the equipment is reduced, the oil-water separation effect is good, the floor area is small, the purely mechanical design, the structure Simple and stable.
本发明在生产工艺中不需添加任何试剂和药品,无二次污染,安装维护简单方便,只要接上进水管、出水管就能使用,无需专人运转维护,只需定期收油即可,适用于一切油种,进油浓度越高效果越好,适用于含有天然石油和石油产品、焦油和焦油分馏物、动植物油等的废水处理中,特别适用于饮食业含油废水的处理。 The invention does not need to add any reagents and medicines in the production process, has no secondary pollution, and is simple and convenient to install and maintain. It can be used as long as it is connected to the water inlet and outlet pipes. It does not need special personnel to operate and maintain, and only needs to collect oil regularly. It is suitable for For all oil types, the higher the oil concentration, the better the effect. It is suitable for the treatment of wastewater containing natural petroleum and petroleum products, tar and tar fractions, animal and vegetable oils, etc., especially suitable for the treatment of oily wastewater in the catering industry.
附图说明:Description of drawings:
图1是本发明的结构示意图。 Fig. 1 is a structural schematic diagram of the present invention.
图中:1-调节池、2-除油罐、3-管路、4-漏斗状沉渣斗、5-排污阀、6-压力控制阀、7-油污水管、8-软管、9-浮体入口、10-阀门、11-油污水入口、12-内罐、13-旋流器、14-斜板除油器、15-压回水入口、16-排水口、17-溢流槽、18-排油口。 In the figure: 1-Regulating tank, 2-Oil removal tank, 3-Pipeline, 4-Funnel-shaped sediment bucket, 5-Drainage valve, 6-Pressure control valve, 7-Oil sewage pipe, 8-Hose, 9-Floating body Inlet, 10-valve, 11-oil and sewage inlet, 12-inner tank, 13-cyclone, 14-slope plate oil remover, 15-pressure return water inlet, 16-drainage port, 17-overflow tank, 18 -Oil drain.
具体实施方式 Detailed ways
下面结合附图和实施例对本发明进一步说明。 The present invention will be further described below in conjunction with the accompanying drawings and embodiments.
参见图1,一种地沟油分离装置,有调节池1、除油罐2和连接管路3,所述调节池底部设有漏斗状沉渣斗4,在每个漏斗状沉渣斗4的底部安装有排污阀5,由45度角构成漏斗状沉渣斗4,这样一方面易于清洗,另一方面是防止水流的紊流将大量的泥沙等渣物带入后序的处理设备;在调节池1底下部安装有压力控制阀6和油污水管7,压力控制阀6能稳定液位,使水流入后序的处理设备获得一个不至于太大的流量,以免超过后序设备的处理能力,同时也做到当日排量特大的时候有泄水的作用;所述油污水管7的内端通过软管8连接有浮体入口9,不管油污水水位高低,浮体入口9始终保持在油污水最上层,以便更好地吸收上层的油污水;所述油污水管7外端安装有阀门10和连接有管路3,其中的水阀10,起到关闭水流的作用。当后序处理设备要清洗、维修或更换零部件等就可以关闭水流进行操作;其中的管路3与上述除油罐2底部的油污水入口11相接;所述油污水入口11通过管路3与安装在除油罐2的内腔中内罐12上的旋流器13相通,当含油污水从旋流器13出水口切向上流出,在罐内形成涡流,这时水中浮油很容易由于密度差的作用首先上浮到油层,粒径不是很大的可以借助水流向上的分速度也较快的到达油层,并与油层粘成一体,一部分粒径较小的油粒当它体积小于80~100μm时油粒上浮速度很慢,甚至没有能力上浮,这一部分的油粒在涡旋的水流产生的向心力的作用不断的向中心聚合,油粒都往中心运动的同时彼此之间相互碰撞的几率大大的提高,不断的碰撞聚结成大油粒而上浮,受向心力作用的油珠会在内腔的外壁(亲油材料)表面润湿吸附着,这样材料表面几乎被油包住,直到饱和,再流来的油珠也更容易润湿附着在表面上,附着的油珠不断聚结扩大,并形成油膜,由于浮力和水流冲击的作用,油膜开始脱落到水中形成油珠,自动上浮到油层中,这种亲油性材料可为聚丙烯塑料,这就是石油工业上常用的“润湿聚结”;所述内罐12外周与除油罐内腔壁之间安装有斜板除油器14,斜板除油器14它属于物理法除油,是一种重力分离技术。重力分离法处理含油污水,是根据油和水的密度不同,利用油和水的密度差使油上浮,达到油水分离目的。所述内罐12底部设有压回水15入口,所述内罐14上部设有排水口16,该排水口16连接管路穿过除油罐2罐体与外面相通,所述除油罐2的上部设有溢流槽17,在溢流槽17底部设有排油口18。如图所示,当除油罐2内经油水分离后的油高于溢流堰时就从溢流槽17的排油口18流出;分离后的污水经内罐底部的压回水入口进入内罐内经排水口罐体外,所述除油罐的底部设有排污泥口19。
Referring to Fig. 1, a kind of sewer oil separation device has adjusting tank 1, degreasing
本发明是一种效率高、能耗低、成本、工艺简单的地沟油分离收集装置,整个装置主要分为调节池、除油罐两个部分,收集后由专门收购公司进行收购,可将地沟油转变成高效的生物柴油,不仅有效的缓解了石油紧缺的压力,生物柴油作为燃料还降低对空气的污染。 The present invention is a sewer oil separation and collection device with high efficiency, low energy consumption, low cost and simple process. The whole device is mainly divided into two parts: a regulating tank and an oil removal tank. The conversion of oil into high-efficiency biodiesel not only effectively alleviates the pressure of oil shortage, but also reduces air pollution as a fuel.
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| Application Number | Priority Date | Filing Date | Title |
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| CN2012100957199A CN102603032A (en) | 2012-04-03 | 2012-04-03 | Waste oil separation device |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012100957199A CN102603032A (en) | 2012-04-03 | 2012-04-03 | Waste oil separation device |
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| CN102603032A true CN102603032A (en) | 2012-07-25 |
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| CN2012100957199A Pending CN102603032A (en) | 2012-04-03 | 2012-04-03 | Waste oil separation device |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103159362A (en) * | 2012-12-27 | 2013-06-19 | 周鼎力 | Three-phase separation and waste water purification standard treatment device of kitchen waste including 'waste oil' and solid waste and kitchen waste water |
| CN103977628A (en) * | 2014-03-26 | 2014-08-13 | 嘉兴市绿能废弃油脂回收有限公司 | Separation method for oil-water slag generated during refining of swill-cooked dirty oil |
| CN119912129A (en) * | 2025-04-03 | 2025-05-02 | 山东禧龙石油装备有限公司 | A coalescing filter tank for treating oily wastewater |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2521212Y (en) * | 2001-09-03 | 2002-11-20 | 中国石油天然气股份有限公司 | A kind of oily wastewater treatment device |
| CN101823798A (en) * | 2010-05-11 | 2010-09-08 | 江苏元宏科技发展有限公司 | Oily water treatment system of hydropower station |
| CN102153165A (en) * | 2011-04-20 | 2011-08-17 | 扬州澄露环境工程有限公司 | Cyclone air flotation oil-water separator |
| CN102320679A (en) * | 2011-06-22 | 2012-01-18 | 浙江大学 | The whirlwind-type corrugated plate intercepter |
-
2012
- 2012-04-03 CN CN2012100957199A patent/CN102603032A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2521212Y (en) * | 2001-09-03 | 2002-11-20 | 中国石油天然气股份有限公司 | A kind of oily wastewater treatment device |
| CN101823798A (en) * | 2010-05-11 | 2010-09-08 | 江苏元宏科技发展有限公司 | Oily water treatment system of hydropower station |
| CN102153165A (en) * | 2011-04-20 | 2011-08-17 | 扬州澄露环境工程有限公司 | Cyclone air flotation oil-water separator |
| CN102320679A (en) * | 2011-06-22 | 2012-01-18 | 浙江大学 | The whirlwind-type corrugated plate intercepter |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103159362A (en) * | 2012-12-27 | 2013-06-19 | 周鼎力 | Three-phase separation and waste water purification standard treatment device of kitchen waste including 'waste oil' and solid waste and kitchen waste water |
| CN103977628A (en) * | 2014-03-26 | 2014-08-13 | 嘉兴市绿能废弃油脂回收有限公司 | Separation method for oil-water slag generated during refining of swill-cooked dirty oil |
| CN103977628B (en) * | 2014-03-26 | 2016-02-10 | 嘉兴市绿能废弃油脂回收有限公司 | The separation method of oil-water residue in a kind of waste oil extractive process |
| CN119912129A (en) * | 2025-04-03 | 2025-05-02 | 山东禧龙石油装备有限公司 | A coalescing filter tank for treating oily wastewater |
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Application publication date: 20120725 |
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